EP1137797B1 - Expression system for factor viii - Google Patents

Expression system for factor viii Download PDF

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Publication number
EP1137797B1
EP1137797B1 EP99966068A EP99966068A EP1137797B1 EP 1137797 B1 EP1137797 B1 EP 1137797B1 EP 99966068 A EP99966068 A EP 99966068A EP 99966068 A EP99966068 A EP 99966068A EP 1137797 B1 EP1137797 B1 EP 1137797B1
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Prior art keywords
protein
factor viii
cells
fviii
derived
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German (de)
English (en)
French (fr)
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EP1137797A4 (en
EP1137797A1 (en
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Myung-Sam Cho
Sham Yuen Chan
William Kelsey
Helena Yee
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Bayer Corp
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Bayer Corp
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    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
    • C12N5/10—Cells modified by introduction of foreign genetic material
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07K—PEPTIDES
    • C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
    • C07K14/435—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from animals; from humans
    • C07K14/745—Blood coagulation or fibrinolysis factors
    • C07K14/755—Factors VIII, e.g. factor VIII C (AHF), factor VIII Ag (VWF)
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00—Drugs for disorders of the blood or the extracellular fluid
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P7/00—Drugs for disorders of the blood or the extracellular fluid
    • A61P7/04—Antihaemorrhagics; Procoagulants; Haemostatic agents; Antifibrinolytic agents
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K38/00—Medicinal preparations containing peptides
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N2799/00—Uses of viruses
    • C12N2799/02—Uses of viruses as vector
    • C12N2799/021—Uses of viruses as vector for the expression of a heterologous nucleic acid
    • C12N2799/028—Uses of viruses as vector for the expression of a heterologous nucleic acid where the vector is derived from a herpesvirus

Definitions

  • the present invention relates to an improved production method for factor VIII and its derivatives.
  • the method relates generally to vector construction, transfection, and selection of cell lines with enhanced productivity under protein-free conditions.
  • this invention relates to a process for preparing a protein with factor VIII procoagulant activity on an industrial scale.
  • Factor VIII has a domain organization of A1-A2-B-A3-C1-C2 and is synthesized as a single chain polypeptide of 2351 amino acids, from which a 19-amino acid signal peptide is cleaved upon translocation into the lumen of the endoplasmic reticulum. Due to the fact that factor VIII is heavily glycosylated, high-level expression (>0.2 pg/c/d) of factor VIII has been difficult to achieve ( Lind et al., 1995, Eur J Biochem. 232: 19-27 ; Kaufman et al., 1989, Mol Cell Biol. 9: 1233-1242 ).
  • factor VIII in mammalian cells is typically 2-3 orders of magnitude lower than that observed with other genes using similar vectors and approaches.
  • productivity of production cell lines for factor VIII has been in the range of 0.6 -1 ⁇ U/c/d (0.1 - 0.2 pg/c/d).
  • a process for the production of proteins having factor VIII procoagulant activity at the industrial scale Using a newly created cell host, cell clones with specific productivities in the range of 2-4 pg/cell/day (10 - 20 ⁇ U/c/d) were derived. Under serum-free conditions, one clone has sustained a daily productivity of 2 - 4 pg/c/d. Clones with this high level of productivity are able to produce 3 - 4 million units per day in a 15-liter perfusion fermenter.
  • One unit of factor VIII activity is by definition the activity present in one milliliter of plasma.
  • One pg of factor VIII is generally equivalent to about 5 ⁇ U of FVIII activity.
  • a protein having factor VIII procoagulant activity is a protein which causes the activation of Factor X in an in vitro or in vivo model system.
  • this definition includes full length recombinant human factor VIII and the B domain deleted factor VIII whose sequence is described in figure 1 .
  • a high level of expression of a protein having factor VIII procoagulant activity means at least about 2 ⁇ U/c/d, or more preferably at least about 4 ⁇ U/c/d, or most preferably at least about 5 ⁇ U/c/d, of factor VIII activity if grown in plasma derived protein-free medium, or at least about 4 ⁇ U/c/d, or more preferably at least about 8 ⁇ U/c/d, or most preferably at least about 10 ⁇ U/c/d, of factor VIII activity if grown in medium supplemented with plasma derived protein.
  • the protein expressed is BDD-FVIII
  • cell lines having specific productivities up to about 1 5 ⁇ U/c/d, more preferably up to about 20 ⁇ U/c/d may be obtained by the method described herein.
  • derived from is intended to include, but not be limited to, normal mitotic cell division and processes such as transfections, cell fusions, or other genetic engineering techniques used to alter cells or produce cells with new properties.
  • factor VIII derivatives obtained from recombinant gene expression in methotrexate (MTX)-resistant cel! populations was measured by a chromogenic assay. Activity was quantitated using Coatest® factor VIII:C/4 kit (Cromogenix, Molndal, Sweden) according to manufacturer's instructions. A U.S. standard anti-hemophilic factor (factor VIII) known as MEGA 1 (Office of Biologics Research and Review, Bethesda, MD) was used as the standard of measurement in this assay. See Barrowcliffe, 1993, Thromb Haem 70: 876 .
  • BDD FVIII The sequence of the B-domain deleted (BDD) FVIII is shown in Figure 1 .
  • the 90-kD and 80-kD chains were linked by a linker consisting of 14 amino acids. See Chan, S.-Y., "Production of Recombinant Factor VIII in the Presence of Liposome-like Substances of Mixed Composition," U.S. Patent Application No. 08/634,001, filed April 16, 1996 .
  • the expression vector for BDD-FVIII was made using standard recombinant DNA techniques.
  • the structure of the expression vector (pCIS25DTR) is shown in Figure 3 .
  • the vector includes a transcriptional unit for BDD-FVIII and a selectable marker, dihydrofolate reductase (dhfr).
  • a terminal repeat sequence from Epstein-Barr virus which shows enhanced drug selection ratio
  • Figure 2 was inserted into the vector to increase the integration efficiency.
  • the vector is essentially a construct of a vector (deposited ATCC 98879) which has been engineered to include a transcriptional unit corresponding to the sequence shown in figure 1 . Further information about the terminal repeat sequence can be found in the related patent application, to Cho and Chan designated MSB-7254, "Terminal repeat sequence of Epstein-Barr virus enhances drug selection ratio," filed on the same day as the current application.
  • Similar vectors can be constructed and used by those having skill in the art to obtain cells expressing proteins having factor VIII procoagulant activity.
  • coding sequences coding for known variants of factor VIII which retain procoagulant activity can be substituted for the BDD-FVIII coding sequence.
  • other selectable markers can be used, such as glutamine synthetase (gs) or multidrug-resistance gene (mdr).
  • gs glutamine synthetase
  • mdr multidrug-resistance gene
  • the choice of a selection agent must be made accordingly, as is known in the art, i.e. for dhfr, the preferred slection agent is methotrexate, for gs the preferred selection agent is methionine sulfoximine, and for mdr the preferred selection agent is colchicine.
  • HKB11 ATCC deposit no. CRL 12568 - a hybrid of 293S cells and human Burkitt's lymphoma cells, see U.S. Patent application to Cho et al. filed on the same day as the current application and designated MSB-7241, incorporated herein by reference
  • HKB11 ATCC deposit no. CRL 12568 - a hybrid of 293S cells and human Burkitt's lymphoma cells, see U.S. Patent application to Cho et al. filed on the same day as the current application and designated MSB-7241, incorporated herein by reference
  • CHO Choinese hamster ovary
  • 293S human embryonic kidney
  • Amplification of transfected cells was done with increasing methotrexate (MTX) concentrations (100nM, 200nM, 400nM, and 800nM) at 1 x 10 6 cells per 96 well plate in a MTX-selection medium lacking hypoxanthine and thymidine (DME/F12 media without hypoxanthine and thymidine plus 5% dialyzed fetal bovine serum from Hyclone, Logan, UT).
  • MTX resistant cells were scored for growth, and secretion of the BDD-FVIII was screened using a Coatest ® factor VIII kit about 2 - 3 weeks post-transfection. The cultivation of cells were done at 37°C in a humidified 5% CO 2 incubator.
  • Single cell clones were derived by limiting dilution cloning (LDC) of high producing populations in 96 well plates under serum-free conditions.
  • Cells were seeded at 1 - 10 cells per well in DME/F12 media supplemented with Humulin ® recombinant insulin (Lilly, Indianapolis, IN) at 10 ⁇ g/ml, 10X essential amino acids (Life Technology, Gaithersburg, MD), and Plasmanate ® human plasma protein fraction (Bayer, Clayton, NC).
  • Plasmanate ® human plasma protein (HPP) fraction contains human albumin (88%) and various globulins (12%).
  • the clones were screened for BDD-FVIII productivity using the Coatest ® factor VIII kits.
  • the highest producing clones were selected for stability evaluation in shake flasks.
  • the first round LDC was performed using selection medium supplemented with 5% dialyzed FBS.
  • the second round LDC was done in serum-free but Plasmanate ® HPP fraction-containing medium using the first SCC adapted in serum-free medium supplemented with Plasmanate ® HPP fraction.
  • the initial population 1C10 was derived from the HKB cells transfected with pCIS25DTR after amplification with 400 nM MTX in the selection medium with 5% FBS.
  • One of the first single cell clones (SCCs), 10A8, derived from 1C10 by a LDC using a selection medium supplemented with 5% FBS was adapted in serum-free medium supplemented with Plasmanate ® HPP faction.
  • 10A8 showed extremely increased levels of rFVIII production at this stage ( Figure 4b ). Therefore, we did a second LDC using the medium supplemented with Plasmanate ® HPP fraction.
  • the productivity of SCCs e.g.
  • 20B8 derived from the second LDC was similar with Plasmanate ® HPP fraction-adapted 10A8. 20B8 showed higher levels of BDD-FVIII than original 10A8 derived from the first LDC in serum-containing medium. Finally, 20B8 was adapted to growth in plasma protein-free (PPF) medium. Samples of 20B8 were deposited at the American Type Culture Collection (Manassas, VA) (ATCC deposit no. CRL-12582).
  • HKB clones exhibit superior productivity for BDD-FVIII.
  • a 10 - 20 fold increase in productivity was observed in HKB cells when compared to clones derived from transfected CHO and 293S cells.
  • HKB cells which do not form large aggregates of cells when grown in suspension culture, are preferred cells for the expression of proteins having factor VIII procoagulant activity.
  • HKB clones that have been adapted to grow as serum-free suspension cultures were further weaned of plasma protein supplements.
  • the weaning was done in sterile polycarbonate shake flasks (Corning, Corning, NY) at a cell density of about 0.5 x 10 6 cells/ml using plasma derived protein free medium.
  • the plasma protein free (PPF) medium was DME/F12 medium supplemented with pluronic F68 (0.1 %), CuSO 4 (50 nM), and FeSO 4 /EDTA (50 ⁇ M).
  • PPF plasma protein free
  • the productivity of clone 20B8 was evaluated in a 15-liter perfusion fermenter.
  • the fermenter was seeded with clone 20B8 cells at a density of about 3 x 10 6 cells/ml.
  • the fermenter was perfused at a rate of 4 volumes per day with the serum-free production medium as described in the preceding paragraph.
  • a final cell density of 2 x 10 7 cells/ml was sustained throughout the evaluation period (45 days).
  • clone 20B8 was perfused with the serumfree production medium supplemented with Plasmanate ® HPP fraction and was able to sustain high productivity.
  • the cells were perfused with the same serumfree production medium but without Plasmanate ® HPP fraction. As shown in Figure 5 , the cells continued to produce high levels of FVIII in a plasma derived protein-free environment. "Plasma derived protein-free" means that essentially no proteins isolated from plasma have been added to the medium.
  • HKB cells provide a protein-free production system to produce not only BDD-FVIII but other therapeutic proteins as well. Proteins produced from HKB cells have human glycosylation patterns which may improve the half-life of certain glycoproteins in vivo. These cells should also be useful for the production of adenovirus and adeno-associated virus strains that have been designed for gene therapy purposes.

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EP99966068A 1998-12-10 1999-12-08 Expression system for factor viii Expired - Lifetime EP1137797B1 (en)

Applications Claiming Priority (3)

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US209916 1998-12-10
US09/209,916 US6358703B1 (en) 1998-12-10 1998-12-10 Expression system for factor VIII
PCT/US1999/029169 WO2000034505A1 (en) 1998-12-10 1999-12-08 Expression system for factor viii

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EP1137797A1 EP1137797A1 (en) 2001-10-04
EP1137797A4 EP1137797A4 (en) 2005-06-22
EP1137797B1 true EP1137797B1 (en) 2008-10-29

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JP (1) JP4240818B2 (sk)
KR (1) KR100616028B1 (sk)
AT (1) ATE412765T1 (sk)
AU (1) AU761801B2 (sk)
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BR (1) BRPI9916069B8 (sk)
CA (1) CA2354845C (sk)
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DE (1) DE69939839D1 (sk)
DK (1) DK1137797T3 (sk)
ES (1) ES2315026T3 (sk)
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IL (2) IL143353A0 (sk)
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CN116731201A (zh) 2014-01-10 2023-09-12 比奥贝拉蒂治疗公司 因子viii嵌合蛋白及其用途
EP3331608A4 (en) 2015-08-03 2019-05-01 Bioverativ Therapeutics Inc. FUSION XI FUSION PROTEINS AND METHODS OF MAKING AND USING THE SAME
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US9249209B2 (en) 2016-02-02
US20020102730A1 (en) 2002-08-01
SK286945B6 (sk) 2009-08-06
US6358703B1 (en) 2002-03-19
IL143353A (en) 2010-12-30
CA2354845A1 (en) 2000-06-15
TR200101592T2 (tr) 2001-11-21
HUP0200558A2 (en) 2002-06-28
CA2354845C (en) 2008-08-12
HU228489B1 (en) 2013-03-28
NO329544B1 (no) 2010-11-08
CZ302330B6 (cs) 2011-03-16
WO2000034505A1 (en) 2000-06-15
SI20644A (sl) 2002-02-28
PL349284A1 (en) 2002-07-15
NZ512234A (en) 2002-12-20
IL143353A0 (en) 2002-04-21
AU761801B2 (en) 2003-06-12
EP1137797A4 (en) 2005-06-22
ES2315026T3 (es) 2009-03-16
US20090036358A1 (en) 2009-02-05
BG65431B1 (bg) 2008-07-31
NO20012718L (no) 2001-06-01
US20130267468A1 (en) 2013-10-10
AU2170100A (en) 2000-06-26
US20130143818A1 (en) 2013-06-06
NO20012718D0 (no) 2001-06-01
RU2249041C2 (ru) 2005-03-27
PL200676B1 (pl) 2009-01-30
KR20020013481A (ko) 2002-02-20
JP4240818B2 (ja) 2009-03-18
RO121604B1 (ro) 2007-12-28
BRPI9916069B8 (pt) 2021-05-25
HUP0200558A3 (en) 2004-11-29
BRPI9916069B1 (pt) 2016-08-02
BR9916069A (pt) 2001-09-04
ATE412765T1 (de) 2008-11-15
JP2002531137A (ja) 2002-09-24
CZ20012024A3 (cs) 2001-10-17
US8207117B2 (en) 2012-06-26
US8945869B2 (en) 2015-02-03
KR100616028B1 (ko) 2006-08-28
DE69939839D1 (de) 2008-12-11
US20170267745A1 (en) 2017-09-21
SK7922001A3 (en) 2002-01-07
PT1137797E (pt) 2008-12-26
US20030077752A1 (en) 2003-04-24
UA77383C2 (uk) 2006-12-15
SI20644B (sl) 2009-04-30
US20110144025A1 (en) 2011-06-16
EP1137797A1 (en) 2001-10-04
US7459525B2 (en) 2008-12-02
DK1137797T3 (da) 2009-02-23
US9650431B2 (en) 2017-05-16
US20160115219A1 (en) 2016-04-28
US20020115152A1 (en) 2002-08-22
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